Abstract
Different iron carbides were synthesized from the iron oxalate precursor by varying the CO carburization temperature between 320 and 450 °C. These iron carbides were applied to the high-temperature Fischer–Tropsch synthesis (FTS) without in situ activation treatment directly. The iron oxalate as a precursor was prepared using a solid-state reaction treatment at room temperature. Pure Fe5C2 was formed at a carburization temperature of 320 °C, whereas pure Fe3C was formed at 450 °C. Interestingly, at intermediate carburization temperatures (350–375 °C), these two phases coexisted at the same time although in different proportions, and 360 °C was the transition temperature at which the iron carbide phase transformed from the Fe5C2 phase to the Fe3C phase. The results showed that CO conversions and products selectivity were affected by both the iron carbide phases and the surface carbon layer. CO conversion was higher (75–96%) when Fe5C2 was the dominant iron carbide. The selectivity to C5+ products was higher when Fe3C was alone, while the light olefins selectivity was higher when the two components (Fe5C2 and Fe3C phases) co-existed, but the quantity of Fe3C was small.
Highlights
Fischer–Tropsch Synthesis (FTS) technology is a key alternative technology to alleviate the present situation of the oil shortage
The main peak intensity of the IO-350 ◦ C catalyst was stronger than the IO-320 ◦ C one, and the peak position slightly shifted to a high angle, suggesting that the IO-350 ◦ C catalyst was single-phase Fe5 C2, and had a small amount of Fe3 C [21]
When the carburization temperature continued to increase to 375 ◦ C, the catalyst displayed diffraction peaks at 37.76◦, 39.82◦, 40.65◦, 42.89◦, 43.76◦, 45.00◦, 45.88◦ and 49.13◦, which were attributed to Fe3 C (JCPDS, NO. 64-2411)
Summary
Fischer–Tropsch Synthesis (FTS) technology is a key alternative technology to alleviate the present situation of the oil shortage. It is possible to use resources such as coal, natural gas and biomass efficiently for the reaction [1,2,3,4]. Iron-based catalysts were used widely for FTS owing to their numerous advantages such as low price, moderate activity for the Water-Gas Shift reaction, a wide range of applicable temperature and larger space for controlling the ratio of hydrogen to carbon monoxide, etc. Due to the complex phase transitions that occur under pretreatment, as well as under Fischer–Tropsch synthesis reaction conditions, no definitive conclusion was obtained regarding the active phase and the role of iron-based catalysts during the reaction. It is believed that iron carbide is related to the activity of iron-based catalysts for FTS reaction to some extent [8,9,10].
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